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US3069249A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the production of fuel gas low in carbon monoxide

Assignee: GEA Group AG
•
Filing: 1959-03-10
•
Granted: 1962-12-18
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Expires: 1979-03-10
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Abstract

No abstract record available.

Inventors

  • 👤 Herbert Wilhelm
  • 👤 Gross Hans-Werner
  • 👤 Dorschner Oskar

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 13:54
CPC Classifications
C; C10; C10K; C10K3/00; C10K3/02; C10K3/04

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 156 words
A PROCESS FOR DIRECTLY PRODUCING PURIFIED LOW CARBON MONOXIDE CONTENT FUEL GAS OF DENSITY LOWER THAN COKE-OVEN GAS FROM HOT CRUDE FUEL GAS HIGH IN CARBON MONOXIDE AND ATTENDANT IMPURITIES OBTAINED BY PRESSURE GASIFICATION OF SOLID CARBON-CONTAINING FUELS WITH STEAM AND OXYGEN WHICH COMPRISES COOLING SAID HOT CRUDE GAS INCLUDING UNUSED STEAM THEREIN TO A TEMPERATURE OF FROM ABOUT 160 TO 2000*C. UNDER PRESSURE TO SEPARATE IMPURITIES SSUCH AS HIGH BOILING HYDROCARBON FRACTIONS, IOLS TARS AND DUST, REMOVING SAID IMPURITIES FOR SAID CRUDE GAS AND SAID UNUSED STEAM, HEATING THE COOLED CRUDE GAS AND SAID UNUSED STEAM TO A TEMPERATURE BETWEEN 250 AND 400*C., CONDUCTING THE HEATED CRUDE GAS AND SAID UNUSED STEAM OVER A CONVERSION CATALYST TO CONVERT THE HIGH CARBON MONOXIDE CONTENT AND STEAM UNUSED IN THE PRESSURE GASIFICATION TO CARBON DIOXIDE AND HYDROGEN SUBSTANTIALLY REMOVING RESIN-FORMERS AND SULPHUR COMPOUNDS DURING SAID CONVERSION, AND THEREAFTER RECOVERING THE PURIFIED LOWER CARBON MONOXIDE CONTENT FUEL GAS.
Claim 2
Dependent Claim 156 words
A PROCESS FOR DIRECTLY PRODUCING PURIFIED LOW CARBON MONOXIDE CONTENT FUEL GAS OF DENSITY LOWER THAN COKE-OVEN GAS FROM HOT CRUDE FUEL GAS HIGH IN CARBON MONOXIDE AND ATTENDANT IMPURITIES OBTAINED BY PRESSURE GASIFICATION OF SOLID CARBON-CONTAINING FUELS WITH STEAM AND OXYGEN WHICH COMPRISES COOLING SAID HOT CRUDE GAS INCLUDING UNUSED STEAM THEREIN TO A TEMPERATURE OF FROM ABOUT 160 TO 2000*C. UNDER PRESSURE TO SEPARATE IMPURITIES SSUCH AS HIGH BOILING HYDROCARBON FRACTIONS, IOLS TARS AND DUST, REMOVING SAID IMPURITIES FOR SAID CRUDE GAS AND SAID UNUSED STEAM, HEATING THE COOLED CRUDE GAS AND SAID UNUSED STEAM TO A TEMPERATURE BETWEEN 250 AND 400*C., CONDUCTING THE HEATED CRUDE GAS AND SAID UNUSED STEAM OVER A CONVERSION CATALYST TO CONVERT THE HIGH CARBON MONOXIDE CONTENT AND STEAM UNUSED IN THE PRESSURE GASIFICATION TO CARBON DIOXIDE AND HYDROGEN SUBSTANTIALLY REMOVING RESIN-FORMERS AND SULPHUR COMPOUNDS DURING SAID CONVERSION, AND THEREAFTER RECOVERING THE PURIFIED LOWER CARBON MONOXIDE CONTENT FUEL GAS.

References Cited (Backward Citations)

US2465235A Cited
US1330772A Cited
US1834115A Cited
US2338402A Cited
US2865864A Cited
US2892685A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1965-12-17 1966-06-18 1966-12-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1969-12-17 1970-06-18 1970-12-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1973-12-17 1974-06-18 1974-12-18 $7700.00 Window Closed / Lapsed

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